Alkylation of mixed olefins with isobutane in a stratco chemical reactor
Conference
·
OSTI ID:416424
- ABB Lummus Global Inc., Houston, TX (United States)
- Lamar Univ., Beaumont, TX (United States)
- Louisiana State Univ., Baton Rouge, LA (United States)
The 17 reaction model for the sulfuric acid alkylation of isobutane with propylene as proposed by Langley and Pike has been used to simulate the effluent refrigeration reactor. The simulation conditions selected to minimize the formation of light and heavy by-product were determined to be: Temperature: 9 - 10 {degrees}C,- Isobutane/Olefin Ratio: 8 - 10; % Volume of Acid: 50 %. The reactor effluent composition from the simulation program has been used to compare with several sets of published data with reasonable agreement. This model has been extrapolated to simulate the alkylation of isobutane with butylenes and amylenes. The model will be optimized with commercial data. 9 refs., 6 figs., 1 tab.
- OSTI ID:
- 416424
- Report Number(s):
- CONF-960730--
- Country of Publication:
- United States
- Language:
- English
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